US9181155B2 - Process for synthesis of alcohols - Google Patents
Process for synthesis of alcohols Download PDFInfo
- Publication number
- US9181155B2 US9181155B2 US14/376,604 US201214376604A US9181155B2 US 9181155 B2 US9181155 B2 US 9181155B2 US 201214376604 A US201214376604 A US 201214376604A US 9181155 B2 US9181155 B2 US 9181155B2
- Authority
- US
- United States
- Prior art keywords
- alcohol
- synthesis gas
- phase
- alcohols
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000000034 method Methods 0.000 title claims abstract description 12
- 230000015572 biosynthetic process Effects 0.000 title claims description 28
- 238000003786 synthesis reaction Methods 0.000 title claims description 28
- 150000001298 alcohols Chemical class 0.000 title claims description 13
- 239000007789 gas Substances 0.000 claims abstract description 38
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000000047 product Substances 0.000 claims abstract description 16
- 238000005984 hydrogenation reaction Methods 0.000 claims abstract description 13
- 150000002576 ketones Chemical class 0.000 claims abstract description 13
- 150000001299 aldehydes Chemical class 0.000 claims abstract description 12
- 239000006227 byproduct Substances 0.000 claims abstract description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 8
- 239000001257 hydrogen Substances 0.000 claims abstract description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- 238000010926 purge Methods 0.000 claims abstract description 4
- 239000003054 catalyst Substances 0.000 claims description 20
- 239000012071 phase Substances 0.000 claims description 16
- 150000002148 esters Chemical class 0.000 claims description 10
- 239000007791 liquid phase Substances 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 5
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 229910000510 noble metal Inorganic materials 0.000 claims description 3
- 239000001569 carbon dioxide Substances 0.000 claims description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 claims description 2
- 150000002431 hydrogen Chemical class 0.000 claims description 2
- 239000012263 liquid product Substances 0.000 claims description 2
- 238000004064 recycling Methods 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- 230000003197 catalytic effect Effects 0.000 abstract description 2
- -1 ester compounds Chemical class 0.000 abstract 1
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 9
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 6
- 239000010949 copper Substances 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 229940032007 methylethyl ketone Drugs 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- TZIHFWKZFHZASV-UHFFFAOYSA-N methyl formate Chemical compound COC=O TZIHFWKZFHZASV-UHFFFAOYSA-N 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910018054 Ni-Cu Inorganic materials 0.000 description 1
- 229910018481 Ni—Cu Inorganic materials 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 125000003718 tetrahydrofuranyl group Chemical group 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C27/00—Processes involving the simultaneous production of more than one class of oxygen-containing compounds
- C07C27/04—Processes involving the simultaneous production of more than one class of oxygen-containing compounds by reduction of oxygen-containing compounds
- C07C27/06—Processes involving the simultaneous production of more than one class of oxygen-containing compounds by reduction of oxygen-containing compounds by hydrogenation of oxides of carbon
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/147—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof
- C07C29/149—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof with hydrogen or hydrogen-containing gases
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B41/00—Formation or introduction of functional groups containing oxygen
- C07B41/02—Formation or introduction of functional groups containing oxygen of hydroxy or O-metal groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/1516—Multisteps
- C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/88—Separation; Purification; Use of additives, e.g. for stabilisation by treatment giving rise to a chemical modification of at least one compound
- C07C29/90—Separation; Purification; Use of additives, e.g. for stabilisation by treatment giving rise to a chemical modification of at least one compound using hydrogen only
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
- C07C31/04—Methanol
Definitions
- the invention relates to a process for production of alcohols from alcohol synthesis gas.
- the invention concerns purification of alcohols by conversion of ketones, aldehydes and esters present in the alcohols in presence of one or more catalysts being active in the conversion of ketones, esters, aldehydes and hydrogen to alcohols.
- the present invention provides a process for production of alcohol product, comprising the steps of
- step (c) cooling and separating the crude alcohol product withdrawn from step (b) into a gas phase comprising hydrogen, carbon monoxide and carbon dioxide and into a liquid product comprising the one or more alcohols and by-products comprising ketones, esters and aldehydes formed in the conversion of the alcohol synthesis gas;
- step (d) purging a part of the gas phase obtained in step (c) and recycling the remaining gas phase to step (a);
- step (e) prior to introduction of the remaining gas phase into step (a) mixing the recycled remaining gas phase product with fresh synthesis gas to form the alcohol synthesis gas;
- step (f) subsequent to the cooling and separation in step (c) withdrawing the liquid phase and subjecting the liquid phase to a two phase catalytic hydrogenation of the ketones, esters and aldehydes by-products to corresponding alcohols,
- liquid phase is hydrogenated with the part of the gas phase being purged from step (d).
- Catalysts for use in the alcohol synthesis and hydrogenation ketones, esters and aldehydes are known per se in the art.
- n CO+2 n H 2 CnH 2n+1 OH+( n ⁇ 1) H 2 O (1).
- the oxo-compound by-products such as acetone and methyl-ethyl ketone etc are formed in small quantities during alcohol synthesis.
- catalysts for the hydrogenation contain noble metal including Pt and Pd.
- Base metal catalysts like a 10 wt % Ni—Cu catalyst have been mentioned in the art.
- U.S. Pat. No. 5,243,095 discloses a Cu, Fe, Mn, Al based catalyst for ketone hydrogenation and U.S. Pat. No. 3,925,490 claims a Cu, Cr catalyst.
- the Cu content in the Cu-containing hydrogenation catalysts is in the range of 10-95% by weight, preferably 40-70% by weight.
- the catalyst can be in form of pellets, extrudates or powder.
- FIG. 1 of the drawings shows a simplified flow sheet of a process according to an embodiment of the invention.
- alcohol synthesis gas is formed by mixing fresh synthesis gas 1 comprising carbon monoxide and hydrogen with recycle gas 2 .
- the formed synthesis gas 3 is introduced into alcohol synthesis reactor system 4 .
- the crude alcohol product from 5 from the alcohol synthesis reactor system 4 contains methanol, unconverted alcohol synthesis gas and traces of ketones, esters and aldehydes.
- the crude alcohol product 5 is cooled (not shown).
- the cooled product is then separated in the separator into a vapour and liquid phase, 7 and 8 respectively.
- a part of the gas phase is purged through line 9 to reduce the amount of inerts accumulating in the synthesis loop (eg. Ar, N2 and CH4).
- the remainder of the gas forms recycle gas stream 2 .
- the liquid stream 8 is passed into two phase hydrogenation reactor 10 .
- Ketones, aldehydes and esters contained in the liquid phase 8 are hydrogenated with purge gas 9 into alcohol in presence of a hydrogenation catalyst.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Process for the catalytic production of alcohol products, wherein by-products comprising ketone, aldehyde and ester compounds contained in the alcohol product are subjected to hydrogenation with a hydrogen-containing purge gas.
Description
The invention relates to a process for production of alcohols from alcohol synthesis gas. In particular the invention concerns purification of alcohols by conversion of ketones, aldehydes and esters present in the alcohols in presence of one or more catalysts being active in the conversion of ketones, esters, aldehydes and hydrogen to alcohols.
During alcohol synthesis from hydrogen and carbon oxides comprising synthesis gas, by-products such as water, aldehydes, esters and ketones are formed frequently. Species like acetone and methyl ethyl ketone with a boiling point close to that of the prepared alcohol are difficult to remove and consequently the presence of these species will contribute to the demand for a larger and more costly distillation column for the purification of the alcohol product.
It is thus a general object of the invention to provide a process for the production of an alcohol product by catalytic conversion of H2, CO and CO2, wherein the produced alcohol product has a substantially reduced content of oxocompounds including aldehyde and ketone impurities.
Thus, the present invention provides a process for production of alcohol product, comprising the steps of
(a) providing an alcohol synthesis gas comprising hydrogen and carbon monoxide;
(b) converting the alcohol synthesis gas into a crude alcohol product stream comprising one or more alcohols and unconverted alcohol synthesis gas in presence of one or more catalysts active in converting the alcohol synthesis gas into the one or more alcohols;
(c) cooling and separating the crude alcohol product withdrawn from step (b) into a gas phase comprising hydrogen, carbon monoxide and carbon dioxide and into a liquid product comprising the one or more alcohols and by-products comprising ketones, esters and aldehydes formed in the conversion of the alcohol synthesis gas;
(d) purging a part of the gas phase obtained in step (c) and recycling the remaining gas phase to step (a);
(e) prior to introduction of the remaining gas phase into step (a) mixing the recycled remaining gas phase product with fresh synthesis gas to form the alcohol synthesis gas; and
(f) subsequent to the cooling and separation in step (c) withdrawing the liquid phase and subjecting the liquid phase to a two phase catalytic hydrogenation of the ketones, esters and aldehydes by-products to corresponding alcohols,
wherein the liquid phase is hydrogenated with the part of the gas phase being purged from step (d).
Catalysts for use in the alcohol synthesis and hydrogenation ketones, esters and aldehydes are known per se in the art.
On a Cu-based catalyst, alcohol is produced from synthesis gas via the following reactions
n CO+2n H2=CnH2n+1OH+(n−1) H2O (1).
n CO+2n H2=CnH2n+1OH+(n−1) H2O (1).
The oxo-compound by-products such as acetone and methyl-ethyl ketone etc are formed in small quantities during alcohol synthesis.
Hydrogenation of these by-products is possible on copper, nickel and/or noble metal based catalysts and follows e.g the reactions:
Methyl formate: C2H4O2+2H2=2CH3OH
Acetone: C3H6O +H2=C3H8O
Methyl ethyl ketone: C4H8O +H2=C3H8O
Particular suitable catalysts for the hydrogenation contain noble metal including Pt and Pd. Base metal catalysts like a 10 wt % Ni—Cu catalyst have been mentioned in the art. E.g. U.S. Pat. No. 5,243,095 discloses a Cu, Fe, Mn, Al based catalyst for ketone hydrogenation and U.S. Pat. No. 3,925,490 claims a Cu, Cr catalyst.
In general, the Cu content in the Cu-containing hydrogenation catalysts is in the range of 10-95% by weight, preferably 40-70% by weight.
The catalyst can be in form of pellets, extrudates or powder.
The crude alcohol product from 5 from the alcohol synthesis reactor system 4 contains methanol, unconverted alcohol synthesis gas and traces of ketones, esters and aldehydes.
The crude alcohol product 5 is cooled (not shown). The cooled product is then separated in the separator into a vapour and liquid phase, 7 and 8 respectively. A part of the gas phase is purged through line 9 to reduce the amount of inerts accumulating in the synthesis loop (eg. Ar, N2 and CH4). The remainder of the gas forms recycle gas stream 2.
The liquid stream 8 is passed into two phase hydrogenation reactor 10. Ketones, aldehydes and esters contained in the liquid phase 8, are hydrogenated with purge gas 9 into alcohol in presence of a hydrogenation catalyst.
Claims (6)
1. A process for production of alcohol product, comprising the steps of:
(a) providing an alcohol synthesis gas comprising hydrogen and carbon monoxide;
(b) converting the alcohol synthesis gas into a crude alcohol product stream comprising one or more alcohols and unconverted alcohol synthesis gas in presence of one or more catalysts active in converting the alcohol synthesis gas into the one or more alcohols;
(c) cooling and separating the crude alcohol product withdrawn from step (b) into a gas phase comprising hydrogen, carbon monoxide and carbon dioxide and into a liquid product comprising the one or more alcohols and by-products comprising ketones, esters and/or aldehydes formed in the conversion of the alcohol synthesis gas;
(d) purging a part of the gas phase obtained in step (c) and recycling the remaining gas phase to step (a);
(e) prior to introduction of the remaining gas phase into step (a) mixing the recycled remaining gas phase product with fresh synthesis gas to farm the alcohol synthesis gas; and
(f) subsequent to the cooling and separation in step (c), withdrawing the liquid phase and subjecting the liquid phase to a two phase catalytic hydrogenation of the ketones, esters and/or aldehydes in the by-products to corresponding alcohols,
wherein the liquid phase is hydrogenated with the part of the gas phase being purged from step (d).
2. Process according to claim 1 , wherein the hydrogenation catalyst is a Cu based catalyst.
3. Process according to claim 2 , wherein the Cu content of the hydrogenation catalyst is in the range of 10-95% by weight.
4. Process according to claim 1 , wherein the hydrogenation catalyst is a noble metal based catalyst.
5. Process according to claim 1 , wherein the hydrogenation of the crude alcohol is performed at a pressure of between 2 and 15 MPa and a temperature between 20° C. and 120° C.
6. Process according to claim 2 , wherein the Cu content of the hydrogenation catalyst is in the range of 40-70% by weight.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DK201200112 | 2012-02-13 | ||
| DKPA201200112 | 2012-02-13 | ||
| DKPA201200112 | 2012-02-13 | ||
| PCT/EP2012/070674 WO2013120548A1 (en) | 2012-02-13 | 2012-10-18 | Process for synthesis of alcohols |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| US20150045460A1 US20150045460A1 (en) | 2015-02-12 |
| US9181155B2 true US9181155B2 (en) | 2015-11-10 |
Family
ID=47045034
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US14/376,604 Expired - Fee Related US9181155B2 (en) | 2012-02-13 | 2012-10-18 | Process for synthesis of alcohols |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US9181155B2 (en) |
| EP (1) | EP2814799A1 (en) |
| KR (1) | KR20140129008A (en) |
| CN (1) | CN104125941B (en) |
| AR (1) | AR089946A1 (en) |
| AU (1) | AU2012370043B2 (en) |
| CA (1) | CA2862522A1 (en) |
| EA (1) | EA024691B9 (en) |
| MX (1) | MX355458B (en) |
| WO (1) | WO2013120548A1 (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB694962A (en) | 1949-06-29 | 1953-07-29 | Stanolind Oil & Gas Co | Improvements in or relating to production of alcohols and organic acids from oxygenated organic compounds |
| WO2004056731A2 (en) | 2002-12-21 | 2004-07-08 | Haldor Topsøe A/S | Process for synthesis of methanol |
| EP1741692A1 (en) | 2005-07-06 | 2007-01-10 | BP Chemicals Limited | Process for the conversion of hydrocarbons to C2-oxygenates |
| WO2007066036A2 (en) | 2005-12-05 | 2007-06-14 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method for synthesising methanol or oxo alcohols used for recycling a residual gas |
| US20110046421A1 (en) * | 2007-11-14 | 2011-02-24 | Bp P.L.C. | Process for the production of alcohol from a carbonaceous feedstock |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1935900C3 (en) | 1969-07-15 | 1975-03-13 | Chemische Werke Huels Ag, 4370 Marl | Process for the removal of aldehydes and ketones from gas streams containing carbon monoxide |
| US5243095A (en) | 1992-04-24 | 1993-09-07 | Engelhard Corporation | Hydrogenation catalyst, process for preparing and process for using said catalyst |
-
2012
- 2012-10-18 MX MX2014009401A patent/MX355458B/en active IP Right Grant
- 2012-10-18 KR KR1020147022356A patent/KR20140129008A/en not_active Ceased
- 2012-10-18 AU AU2012370043A patent/AU2012370043B2/en not_active Ceased
- 2012-10-18 WO PCT/EP2012/070674 patent/WO2013120548A1/en active Application Filing
- 2012-10-18 EA EA201491516A patent/EA024691B9/en not_active IP Right Cessation
- 2012-10-18 US US14/376,604 patent/US9181155B2/en not_active Expired - Fee Related
- 2012-10-18 EP EP12775020.6A patent/EP2814799A1/en not_active Withdrawn
- 2012-10-18 CA CA2862522A patent/CA2862522A1/en not_active Abandoned
- 2012-10-18 CN CN201280069706.2A patent/CN104125941B/en not_active Expired - Fee Related
-
2013
- 2013-02-08 AR ARP130100403A patent/AR089946A1/en unknown
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB694962A (en) | 1949-06-29 | 1953-07-29 | Stanolind Oil & Gas Co | Improvements in or relating to production of alcohols and organic acids from oxygenated organic compounds |
| WO2004056731A2 (en) | 2002-12-21 | 2004-07-08 | Haldor Topsøe A/S | Process for synthesis of methanol |
| EP1741692A1 (en) | 2005-07-06 | 2007-01-10 | BP Chemicals Limited | Process for the conversion of hydrocarbons to C2-oxygenates |
| CN101218197A (en) | 2005-07-06 | 2008-07-09 | 英国石油化学品有限公司 | Processes for the conversion of hydrocarbons to C2-oxygenates |
| US7842844B2 (en) * | 2005-07-06 | 2010-11-30 | Bp Chemicals Limited | Process for the conversion of hydrocarbons to C2-oxygenates |
| WO2007066036A2 (en) | 2005-12-05 | 2007-06-14 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method for synthesising methanol or oxo alcohols used for recycling a residual gas |
| US20110046421A1 (en) * | 2007-11-14 | 2011-02-24 | Bp P.L.C. | Process for the production of alcohol from a carbonaceous feedstock |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104125941A (en) | 2014-10-29 |
| EP2814799A1 (en) | 2014-12-24 |
| WO2013120548A1 (en) | 2013-08-22 |
| CN104125941B (en) | 2016-08-17 |
| US20150045460A1 (en) | 2015-02-12 |
| MX355458B (en) | 2018-04-19 |
| MX2014009401A (en) | 2014-11-10 |
| EA024691B9 (en) | 2018-02-28 |
| AU2012370043B2 (en) | 2017-06-15 |
| KR20140129008A (en) | 2014-11-06 |
| CA2862522A1 (en) | 2013-08-22 |
| EA024691B1 (en) | 2016-10-31 |
| EA201491516A1 (en) | 2015-01-30 |
| AU2012370043A1 (en) | 2014-08-28 |
| AR089946A1 (en) | 2014-10-01 |
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